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CN106283101B - A kind of preparation method of ultra-pure hydrogen - Google Patents

A kind of preparation method of ultra-pure hydrogen Download PDF

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CN106283101B
CN106283101B CN201610752256.7A CN201610752256A CN106283101B CN 106283101 B CN106283101 B CN 106283101B CN 201610752256 A CN201610752256 A CN 201610752256A CN 106283101 B CN106283101 B CN 106283101B
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pure hydrogen
water
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CN106283101A (en
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徐大鹏
杨延河
师富良
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SHANDONG HONGDA BIOTECHNOLOGY CO Ltd
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    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • CCHEMISTRY; METALLURGY
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    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/50Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
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    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465Composition of the impurity
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465Composition of the impurity
    • C01B2203/0475Composition of the impurity the impurity being carbon dioxide
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465Composition of the impurity
    • C01B2203/0495Composition of the impurity the impurity being water
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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Abstract

本发明公开了一种超纯氢的制备方法,本发明采用电解制氢工艺,对电解前的软化水进行预处理,将软化水进行加热,将其中溶解的N2、Ar等各种气体全部脱除,通入高纯氧保压,再经催化剂催化脱氧和分子筛脱水工艺,过滤除尘工艺,钢瓶烘干处理工艺,生产出符合“GBT 3634.2‑2011纯氢、高纯氢和超纯氢”要求超纯氢。本发明的有益效果:成功避开了钯合金扩散膜(管)分离法成本高且生产量小、储氢合金吸放法中氢化物使用寿命短及生产不稳定、低温吸附法需要使用液氮对设备要求高等的缺点,具有生产能耗低、流程效率高,工艺简单、生产稳定等特点。The invention discloses a method for preparing ultra-pure hydrogen. The invention adopts an electrolytic hydrogen production process, pretreats the demineralized water before electrolysis, heats the demineralized water, and dissolves all kinds of gases such as N 2 and Ar in it. Removal, feeding high-purity oxygen to maintain pressure, and then through catalyst catalytic deoxidation and molecular sieve dehydration process, filtration and dust removal process, steel cylinder drying treatment process, to produce ultra- pure hydrogen. The beneficial effects of the present invention: successfully avoid the high cost and small production capacity of the palladium alloy diffusion membrane (tube) separation method, the short service life of the hydride and the unstable production in the hydrogen storage alloy absorption and release method, and the need to use liquid nitrogen in the low temperature adsorption method The disadvantage of high equipment requirements is that it has the characteristics of low production energy consumption, high process efficiency, simple process and stable production.

Description

一种超纯氢的制备方法A kind of preparation method of ultrapure hydrogen

技术领域technical field

本发明涉及氢气的制备方法,具体地说是一种超纯氢的制备方法。The invention relates to a method for preparing hydrogen, in particular to a method for preparing ultra-pure hydrogen.

背景技术Background technique

随着科学技术的发展,对氢气的质量技术要求愈来愈高,需要纯度为99.9999%的超纯氢。超纯氢应用范围极广,它是现代电子、光纤、石化等方面和一些尖端科技上的重要原料;是环境、卫生、飞船、海底实验室、潜艇等大气成分分析测定和星球物质即时测量必须的高纯气源;是半导体集成电路和光导纤维研制生产、集成光学和纳米研究、晶体外延生长等不可或缺的原料;是食品、药品、疾病控制、化学污染、运动员兴奋剂检测、贵金属熔炼、火箭燃料分析等领域开展工作的重要保障。With the development of science and technology, the quality and technical requirements for hydrogen are getting higher and higher, and ultra-pure hydrogen with a purity of 99.9999% is required. Ultra-pure hydrogen has a wide range of applications. It is an important raw material for modern electronics, optical fibers, petrochemicals, and some cutting-edge technologies; It is an indispensable source of high-purity gas for the development and production of semiconductor integrated circuits and optical fibers, integrated optics and nano research, crystal epitaxial growth, etc. , rocket fuel analysis and other fields to carry out an important guarantee for the work.

当前,国内外有三种生产方法,分别为:At present, there are three production methods at home and abroad, namely:

1.钯合金扩散膜(管)分离法。以纯氢为原料,其膜(管)只允许氢及其同位素通过,从而获得超纯氢。该法的膜(管)极为昂贵,生产成本极高,生产量极小。1. Palladium alloy diffusion membrane (tube) separation method. Using pure hydrogen as raw material, its membrane (tube) only allows hydrogen and its isotopes to pass through, so as to obtain ultra-pure hydrogen. The film (tube) of this method is extremely expensive, the production cost is extremely high, and the production volume is extremely small.

2.储氢合金吸放法。在一定温度、压力下,钛系、锆系、稀土系等金属能大量吸收氢气,单位体积吸储的氢气可为相同温度、压力下气态的1000倍,吸气时放热,加热就能够释放获得高压、质好、两大的超纯氢。该法由于氢化物自身很不稳定,易受有害成分毒害,长时间多次反复吸放使用,性能会明显下降。同时,还存在着机械强度问题,目前的储氢合金材料反复吸放,应用次数不多就要更换,成本高。2. Hydrogen storage alloy absorption and release method. Under a certain temperature and pressure, metals such as titanium series, zirconium series, and rare earth series can absorb a large amount of hydrogen gas, and the hydrogen gas absorbed and stored per unit volume can be 1000 times that of the gaseous state at the same temperature and pressure. High-pressure, high-quality, ultra-pure hydrogen with two major components. Because the hydride itself is very unstable in this method, it is easily poisoned by harmful components. If it is used repeatedly for a long time, the performance will obviously decline. At the same time, there is still a problem of mechanical strength. The current hydrogen storage alloy material is repeatedly absorbed and released, and it needs to be replaced after a few applications, which is costly.

3.低温吸附法。此法一般以水电解制得氢,先采用催化吸附工艺制得高纯氢,后将高压高纯氢采用液氮蒸发温度下的低温吸附,除去微量的氮、氧、一氧化碳、二氧化碳、甲烷、水等杂质,获得超纯氢。该法生产超纯氢耗能高,对设备要求高,而且在实际操作过程中对温度控制、液氮的调节还存在问题,使得装置不能正常生产,产品质量很不稳定。3. Low temperature adsorption method. This method generally produces hydrogen by electrolysis of water. First, high-purity hydrogen is produced by catalytic adsorption process, and then high-pressure high-purity hydrogen is adsorbed at low temperature at the evaporation temperature of liquid nitrogen to remove trace impurities such as nitrogen, oxygen, carbon monoxide, carbon dioxide, methane, and water. Obtain ultra-pure hydrogen. The production of ultra-pure hydrogen by this method requires high energy consumption and high equipment requirements. In addition, there are still problems in temperature control and liquid nitrogen adjustment in the actual operation process, which makes the device unable to produce normally and the product quality is very unstable.

针对以上三种超纯氢生产方法存在的不足,一些新型的超纯氢的制备方法已有些报道,方法也不止一种。CN 101691209 A 提供了一种以高压高纯氢为原料,筛选使用北京大学化学院研发,对氮氧吸附容量(尤其对氮)均大、同时可除其他微量杂质,不同一般4A、5A、13X等等吸附剂的pu-8新型吸附剂,并采用过量10倍吸附剂用量、低6倍常用吸附气速、自控在高压下净化杂质等的新工艺及直接罐充洁净超纯氢钢瓶,成功生产超纯氢的新方法。CN 105268282 A公开了一种低温变压吸附制备超纯氢的方法,该方法以电解水纯化后的99.999%高纯氢为原料,将其降温至-30~35℃,然后进入采用四塔式变压吸附法的变压吸附系统,四塔循环实现工业化。这些发明都在原有技术的基础上进行了创新,能够制备符合国标的超纯氢,但是依然存在工艺复杂,投资大,成本高的问题。In view of the shortcomings of the above three ultra-pure hydrogen production methods, some new ultra-pure hydrogen preparation methods have been reported, and there are more than one method. CN 101691209 A Provides a high-pressure high-purity hydrogen as raw material, which is screened and developed by the School of Chemistry of Peking University. It has a large adsorption capacity for nitrogen and oxygen (especially for nitrogen), and can remove other trace impurities at the same time, which is different from general 4A, 5A, 13X, etc. The adsorbent is a new type of pu-8 adsorbent, and adopts a new technology of 10 times excessive adsorbent dosage, 6 times lower common adsorption gas velocity, self-controlled purification of impurities under high pressure, and direct tank filling of clean ultra-pure hydrogen cylinders, successfully producing ultra- A new approach to pure hydrogen. CN 105268282 A discloses a method for preparing ultra-pure hydrogen by low-temperature pressure swing adsorption. The method uses 99.999% high-purity hydrogen purified by electrolysis of water as raw material, cools it down to -30~35°C, and then enters the four-tower pressure swing The pressure swing adsorption system of the adsorption method realizes the industrialization of the four-tower cycle. These inventions have been innovated on the basis of the original technology, and can produce ultra-pure hydrogen that meets the national standard, but there are still problems of complicated process, large investment and high cost.

发明内容Contents of the invention

针对上述制备超纯氢方法存在的问题,本发明采用电解制氢工艺,对电解前的软化水进行预处理,通入高纯氧保压,再利用催化脱氧和分子筛脱水工艺,过滤除尘,钢瓶烘干处理工艺,生产出的超纯氢纯度符合“GBT 3634.2-2011 纯氢、高纯氢和超纯氢”的要求,具有超纯氢产量高、投资少、生产稳定等特点。In view of the problems existing in the above method for preparing ultra-pure hydrogen, the present invention adopts the electrolytic hydrogen production process to pretreat the softened water before electrolysis, introduce high-purity oxygen to maintain pressure, and then use catalytic deoxidation and molecular sieve dehydration processes to filter and remove dust. Drying treatment process, the purity of ultra-pure hydrogen produced meets the requirements of "GBT 3634.2-2011 pure hydrogen, high-purity hydrogen and ultra-pure hydrogen", and has the characteristics of high output of ultra-pure hydrogen, low investment and stable production.

本发明解决其技术问题所采取的技术方案是:The technical scheme that the present invention solves its technical problem to take is:

一种超纯氢的制备方法,包括以下步骤:A method for preparing ultra-pure hydrogen, comprising the following steps:

(1)预热:将软化水罐中的软化水进行预热;(1) Preheating: Preheat the softened water in the softened water tank;

(2)保压:向步骤(1)预热后的软化水罐中通入高纯氧气保压;(2) Pressure maintenance: Introduce high-purity oxygen into the demineralized water tank preheated in step (1) to maintain pressure;

(3)电解:将步骤(2)中的软化水经冷却后通入水电解系统进行电解,产出电解氢;(3) Electrolysis: Cool the softened water in step (2) and pass it into the water electrolysis system for electrolysis to produce electrolytic hydrogen;

(4)催化脱氧:将步骤(3)中产出的电解氢通过脱氧催化塔脱除氧等杂质;(4) Catalytic deoxygenation: the electrolytic hydrogen produced in step (3) is passed through a deoxygenation catalytic tower to remove impurities such as oxygen;

(5)脱水干燥:将步骤(4)除杂后的电解氢经冷却器冷却后用汽水分离器脱除游离水,增压,增压后通过高压汽水分离器,进入分子筛塔除去水分和二氧化碳。(5) Dehydration and drying: the electrolytic hydrogen after removal of impurities in step (4) is cooled by a cooler, and then free water is removed by a steam-water separator, pressurized, and after the pressurization, it passes through a high-pressure steam-water separator and enters a molecular sieve tower to remove water and carbon dioxide .

(6)过滤除尘:步骤(5)脱水干燥的电解氢经过滤器过滤,除去杂质,即得超纯氢。(6) Filtration and dust removal: In step (5), the dehydrated and dried electrolytic hydrogen is filtered through a filter to remove impurities to obtain ultra-pure hydrogen.

所述步骤(1)中,预热温度优选95~100℃,在此温度范围内,Ar、N2、CO、CO2、CH4和Cl2在水中的溶解度几乎为零(见表1、表2),优选预热时间为10~30min,将溶解在其中的Ar、N2、CO、CO2、CH4和Cl2全部去除。In the step (1), the preheating temperature is preferably 95~100°C. Within this temperature range, the solubility of Ar, N 2 , CO, CO 2 , CH 4 and Cl 2 in water is almost zero (see Table 1, Table 2), the preferred preheating time is 10~30min, to remove all Ar, N 2 , CO, CO 2 , CH 4 and Cl 2 dissolved in it.

所述步骤(2)中预热软化水充高纯氧保压,保压压力优选0.02~0.04MPa,边保压边降温冷却,冷却温度优选0~40℃。由于高纯氧的保压作用,避免空气中Ar、N2、CO、CO2、CH4和Cl2再次溶解在软化水中。In the step (2), the preheated demineralized water is filled with high-purity oxygen to maintain the pressure. The pressure is preferably 0.02-0.04 MPa, and the temperature is lowered while maintaining the pressure. The cooling temperature is preferably 0-40°C. Due to the pressure-holding effect of high-purity oxygen, Ar, N 2 , CO, CO 2 , CH 4 and Cl 2 in the air are prevented from being dissolved in demineralized water again.

所述步骤(4)中采用脱氧催化塔,可降低催化脱氧反应的耗能,作为优化的,所述脱氧催化塔所用催化剂为中国科学院大连化学物理研究所研制的催化剂HC-1,所述脱氧催化塔工作温度优选50±20℃,通过该步骤可以进一步去除电解氢中的氧等杂质。The deoxygenation catalytic tower is used in the step (4), which can reduce the energy consumption of the catalytic deoxygenation reaction. As an optimization, the catalyst used in the deoxygenation catalytic tower is the catalyst HC-1 developed by the Dalian Institute of Chemical Physics, Chinese Academy of Sciences. The deoxidation The working temperature of the catalytic tower is preferably 50±20°C, and impurities such as oxygen in the electrolytic hydrogen can be further removed through this step.

所述步骤(5)中采用汽水分离器、高压汽水分离器和分子筛等设备,充分去除电解氢中的水分、二氧化碳等杂质,作为优化的,电解氢增压至15MPa,所述分子筛优选13XAPG分子筛,由两组组成,工作时一组使用,一组再生。In the step (5), equipment such as a steam-water separator, a high-pressure steam-water separator, and molecular sieves are used to fully remove impurities such as moisture and carbon dioxide in the electrolytic hydrogen. As an optimization, the electrolytic hydrogen is pressurized to 15MPa, and the molecular sieve is preferably 13XAPG molecular sieve , consisting of two groups, one for use during work and one for regeneration.

所述步骤(6)进一步对脱水干燥后的电解氢进行机械杂质的去除,使氢的纯度得到进一步的提高。通过步骤(6)获得的超纯氢在压缩充瓶前。对钢瓶进行特殊烘干处理,去除瓶内粉尘和水,抽至真空后进行充装。The step (6) further removes mechanical impurities from the dehydrated and dried electrolytic hydrogen, so that the purity of hydrogen is further improved. The ultra-pure hydrogen obtained through step (6) is compressed before filling the bottle. Carry out special drying treatment on steel cylinders to remove dust and water in the cylinders, and then fill them after pumping to a vacuum.

表1 气体在水中的溶解度Table 1 Solubility of gases in water

表2 氩气(Ar)吸收系数Table 2 Argon (Ar) absorption coefficient

注:吸收系数,是指在气体分压等于101.325KPa时,被1体积水所吸收的该气体体积。Note: The absorption coefficient refers to the gas volume absorbed by 1 volume of water when the gas partial pressure is equal to 101.325KPa.

本发明的有益效果是:本发明研究出一种新型操作简单、行之有效的超纯氢制备方法,成功避开了钯合金扩散膜(管)分离法成本高、储氢合金吸放法中氢化物使用寿命短、低温吸附法需要使用液氮且工艺不稳定等的缺点。在对原料软化水进行预热处理时,N2、Ar、CH4等各种难于去除的杂质即被脱除,经电解后可得到超纯氢,区别于其他方法中先电解生成高纯氢,再将高纯氢进行纯化的工艺路线,具有生产能耗低、流程效率高,工艺简单、成本低等特点。The beneficial effects of the present invention are: the present invention has developed a novel method for preparing ultra-pure hydrogen that is simple to operate and effective, and successfully avoids the high cost of the palladium alloy diffusion membrane (tube) separation method and the high cost of the hydrogen storage alloy absorption and release method. The disadvantages of hydride are short service life, low-temperature adsorption method needs to use liquid nitrogen and the process is unstable. When preheating the demineralized water, various difficult-to-remove impurities such as N 2 , Ar, CH 4 are removed, and ultra-pure hydrogen can be obtained after electrolysis, which is different from other methods in which high-purity hydrogen is generated by electrolysis first, and then The process route of purifying high-purity hydrogen has the characteristics of low production energy consumption, high process efficiency, simple process and low cost.

具体实施方式Detailed ways

以下对本发明的优选实施例进行详细描述,优选实施例中未注明具体条件的实验方法,按照常规条件进行。The preferred embodiments of the present invention are described in detail below, and the experimental methods not indicating specific conditions in the preferred embodiments are carried out according to conventional conditions.

以下实施例使用的主要设备的信息为:2m3软化水罐,该软化水罐中设有加热盘管和冷凝装置;水电解制氢装置:型号:ZDQ-125/1.5,氢气额定产量:125Nm3/h;催化脱氧塔,该催化脱氧塔采用两组电加热装置来保证反应温度:干燥器:包括汽水分离器、高压汽水分离器和分子筛塔,其中分子筛塔为2组,在工作时一组工作,另一组再生。前述未标明具体型号的设备为工业常规设备,由市售购买所得。The information of the main equipment used in the following examples is: 2m 3 demineralized water tank, which is equipped with heating coil and condensing device; water electrolysis hydrogen production device: model: ZDQ-125/1.5, hydrogen rated output: 125Nm 3 /h; catalytic deoxidation tower, the catalytic deoxidation tower uses two sets of electric heating devices to ensure the reaction temperature: Dryer: including steam-water separator, high-pressure steam-water separator and molecular sieve tower, of which there are two groups of molecular sieve towers. One group works and another group regenerates. The aforementioned equipment not marked with a specific model is an industrial conventional equipment purchased from the market.

实施例1Example 1

通过上述生产装置,按下述流程进行高纯氧的制备:Through the above-mentioned production equipment, the preparation of high-purity oxygen is carried out according to the following process:

(1)预热:在常压下将2m3软化水罐中的软化水加热至100℃,加热时间为15min,将溶解在水中Ar、N2、CO、CO2、CH4和Cl2全部除去;(1) Preheating: Heat the softened water in a 2m 3 softened water tank to 100°C under normal pressure for 15 minutes, and dissolve all Ar, N 2 , CO, CO 2 , CH 4 and Cl 2 in the water remove;

(2)保压:向步骤(1)预热后的软化水罐中通入高纯氧气保压,保压压力为0.3MPa,边保压边降温冷却,冷却温度优选30℃,由于高纯氧的保压作用,避免空气中Ar、N2、CO、CO2、CH4和Cl2再次溶解在软化水中。(2) Pressure maintenance: Introduce high-purity oxygen into the demineralized water tank preheated in step (1) to maintain pressure. The pressure is 0.3MPa. The pressure-holding effect of oxygen prevents Ar, N 2 , CO, CO 2 , CH 4 and Cl 2 in the air from being dissolved in demineralized water again.

(3)电解:将步骤(2)中冷却至30℃的软化水通入水电解制氢装置进行电解,产出电解氢,经检测,其中还有水、二氧化碳等杂质。(3) Electrolysis: The demineralized water cooled to 30°C in step (2) is passed into the water electrolysis hydrogen production device for electrolysis to produce electrolytic hydrogen. After testing, there are impurities such as water and carbon dioxide in it.

(4)催化脱氧:将步骤(3)中产出的电解氢引入脱氧催化塔脱,在温度为50±20℃下,采用中国科学院大连化学物理研究所研制的催化剂HC-1进行催化,使电解氢中的杂质氧与氢反应生成水,得到含氢99.999%的电解氢。(4) Catalytic deoxygenation: The electrolytic hydrogen produced in step (3) is introduced into the deoxygenation catalytic tower for deoxidation. At a temperature of 50±20°C, the catalyst HC-1 developed by the Dalian Institute of Chemical Physics, Chinese Academy of Sciences is used for catalysis, so that The impurity oxygen in the electrolytic hydrogen reacts with hydrogen to generate water, and the electrolytic hydrogen containing 99.999% hydrogen is obtained.

(5)脱水干燥:将步骤(4)除杂后的电解氢经冷却器冷却后用汽水分离器脱除游离水,然后增压至15MPa后通过高压汽水分离器,随后进入分子筛塔除去水分和二氧化碳,所述分子筛优选13XAPG分子筛,由两组组成,工作时一组使用,一组再生。(5) Dehydration and drying: the electrolytic hydrogen after the impurity removal in step (4) is cooled by a cooler, and then free water is removed by a steam-water separator, then pressurized to 15MPa, passes through a high-pressure steam-water separator, and then enters a molecular sieve tower to remove water and For carbon dioxide, the molecular sieve is preferably 13XAPG molecular sieve, which consists of two groups, one group is used during work, and the other group is regenerated.

(6)过滤除尘:步骤(5)脱水干燥的电解氧经过滤器过滤,除去机械杂质,即得纯度为99.99995%的超纯氢,其各项指标详见表3。(6) Filtration and dust removal: The dehydrated and dried electrolytic oxygen in step (5) is filtered through a filter to remove mechanical impurities to obtain ultra-pure hydrogen with a purity of 99.99995%. See Table 3 for details of its indicators.

在压缩充瓶前,盛装超纯氢的钢瓶经过特殊烘干处理,去除瓶内粉尘和水,抽至真空后进行充装,生产出瓶装超纯氢。Before compression and bottle filling, the steel cylinder containing ultra-pure hydrogen is specially dried to remove dust and water in the bottle, and then filled after being pumped to a vacuum to produce bottled ultra-pure hydrogen.

表3 实施例测试结果Table 3 Example test results

上述具体实施方式仅是本发明的具体个案,本发明的专利保护范围包括但不限于上述具体实施方式的产品形态和式样,任何符合本发明权利要求书的一种超纯氢的制备方法且任何所属技术领域的普通技术人员对其所做的适当变化或修饰,皆应落入本发明的专利保护范围。The above-mentioned specific embodiments are only specific cases of the present invention. The scope of patent protection of the present invention includes but is not limited to the product form and style of the above-mentioned specific embodiments, any method for preparing ultra-pure hydrogen that meets the claims of the present invention and any Appropriate changes or modifications made by those skilled in the art shall fall within the scope of patent protection of the present invention.

Claims (5)

1. a kind of preparation method of ultra-pure hydrogen, which is characterized in that include the following steps:
(1)Preheating:Softened water in water softener tank is heated to 95 ~ 100 DEG C, preheating time is 10 ~ 30min;
(2)Pressurize:To step(1)It is passed through high purity oxygen gas pressurize in water softener tank after preheating, dwell pressure is 0.02 ~ 0.04MPa cools down in pressurize, and cooling temperature is controlled at 0 ~ 40 DEG C;
(3)Electrolysis:By step(2)In softened water be passed through water electrolysis system after cooling and be electrolysed, output electrolysis hydrogen;
(4)Catalytic deoxidation:By step(3)The electrolysis hydrogen of middle output passes through deoxidation catalytic tower imurity-removal oxygen;
(5)Dehydration and drying:By step(4)Dissociate except the electrolysis hydrogen after impurity is removed after cooler cools down with steam-water separator Water, electrolysis hydrogen are pressurized to 15MPa, and by high-pressure stream-water separator after supercharging, moisture and carbon dioxide are removed into molecular sieve tower;
(6)Dust removal by filtration:Step(5)The electrolysis hydrogen of dehydration and drying is filtered, and removes impurity to get ultra-pure hydrogen.
2. a kind of preparation method of ultra-pure hydrogen according to claim 1, it is characterised in that:The step(4)Deoxidation is catalyzed Tower used catalyst is the catalyst HC-1 that Dalian Inst of Chemicophysics, Chinese Academy of Sciences develops.
3. a kind of preparation method of ultra-pure hydrogen according to claim 1, it is characterised in that:The step(4)Deoxidation is catalyzed Tower operating temperature is controlled at 30 ~ 70 DEG C.
4. a kind of preparation method of ultra-pure hydrogen according to claim 1, it is characterised in that:The step(5)Molecular sieve is 13XAPG molecular sieves.
5. a kind of preparation method of ultra-pure hydrogen according to claim 1, it is characterised in that:The step(6)What is obtained is super Pure hydrogen carries out drying and processing before bottle is filled in compression, to steel cylinder, removes dust and water in bottle, vacuum pumping loading.
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